Geosciences Rennes (UMR CNRS 6118), Universite Rennes 1, Rennes, France.
J Contam Hydrol. 2011 Mar 1;120-121:184-97. doi: 10.1016/j.jconhyd.2010.08.002. Epub 2010 Aug 12.
We investigate the dispersion of a finite amount of solute after it has been injected into the laminar flow occurring in a horizontal smooth fracture of constant aperture. When solute buoyancy is negligible, the dispersion process eventually leads to the well-known asymptotic Taylor-Aris dispersion regime, in which the solute progresses along the fracture at the average fluid velocity, according to a one-dimensional longitudinal advection-dispersion process. This paper addresses more realistic configurations for which the solute-induced density contrasts within the fluid play an important role on solute transport, in particular at small and moderate times. Flow and transport are coupled, since the solute distribution impacts the variations in time of the advecting velocity field. Transport is simulated using (i) a mathematical description based on the Boussinesq approximation and (ii) a numerical scheme based on a finite element analysis. This enables complete characterization of the process, in particular at moderate times for which existing analytical models are not valid. At very short times as well as very long times, the overall downward advective solute mass flow is observed to scale as the square of the injected concentration. The asymptotic Taylor-Aris effective dispersion coefficient is reached eventually, but vertical density currents, which are significant at short and moderate times, are responsible for a systematic retardation of the asymptotic mean solute position with respect to the frame moving at the mean fluid velocity, as well as for a time shift in the establishment of the asymptotic dispersion regime. These delays are characterized as functions of the Péclet number and another non-dimensional number which we call advective Archimedes number, and which quantifies the ratio of buoyancy to viscous forces. Depending on the Péclet number, the asymptotic dispersion is measured to be either larger or smaller than what it would be in the absence of buoyancy effects. Breakthrough curves measured at distances larger than the typical distance needed to reach the asymptotic dispersion regime are impacted accordingly. These findings suggest that, under certain conditions, density/buoyancy effects may have to be taken into consideration when interpreting field measurement of solute transport in fractured media. They also allow an estimate of the conditions under which density effects related to fracture wall roughness are likely to be significant.
我们研究了在水平光滑裂隙中发生的层流中注入有限量溶质后的弥散情况。当溶质浮力可以忽略不计时,弥散过程最终会导致众所周知的泰勒-阿里斯渐近弥散状态,在这种状态下,溶质沿着裂隙以平均流体速度前进,遵循一维纵向对流-弥散过程。本文研究了更实际的配置,其中流体中溶质引起的密度对比对溶质输运起着重要作用,特别是在小时间和中等时间内。由于溶质分布会影响输运过程中的速度场的时变,因此流动和输运是耦合的。利用(i)基于布西内斯克近似的数学描述和(ii)基于有限元分析的数值方案来模拟输运。这使得过程得到了完整的描述,特别是在现有分析模型不适用的中等时间内。在极短时间和极长时间内,观察到整个向下的对流溶质质量流与注入浓度的平方成正比。最终达到渐近泰勒-阿里斯有效弥散系数,但在短时间和中等时间内显著的垂直密度流会导致渐近平均溶质位置相对于以平均流体速度移动的框架的系统延迟,以及渐近弥散状态的建立的时间偏移。这些延迟被特征化为普朗特数和另一个无量纲数的函数,我们称之为对流阿基米德数,它量化了浮力与粘性力的比值。根据普朗特数,测量到的渐近弥散要么大于,要么小于没有浮力影响时的弥散。在距离大于达到渐近弥散状态所需的典型距离的位置处测量的突破曲线也受到相应的影响。这些发现表明,在某些条件下,在解释裂隙介质中溶质输运的现场测量时,可能需要考虑密度/浮力效应。它们还允许估计与裂隙壁粗糙度相关的密度效应可能显著的条件。